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EFFECTS OF OBSTACLES ON THE MIXING PERFORMANCE IN MICROCHANNELS

机译:障碍物对微通道混合性能的影响

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The mixing of two or more fluid streams in microchannels needs quite long channel lengths. Therefore, in order to improve the mixing performance, obstacles have been placed in the channel to disrupt flow and to reduce the diffusion path. The disruption to flow velocity field alters the flow direction from one fluid to another. Properly designed geometric parameters, such as layout, angle with main flow direction and aspect ratio of obstacles, will be resulted in improving the mixing performance with only little increase of the pressure drop. In this study, T-type rectangular microchannel is used, which has two inlets with W×H×L=100×100×1000 μm~ and one outlet with W×H×L=200× 100×6950 μm~3. Furthermore, the mixing channel has obstacles which are placed with an angle of inclination and with dimensions W×H×L=10×100×h μm~3 on the lower layer. In order to estimate the performance of the mixing, numerical analyses are carried out with water and ethanol. Especially, the diffusion coefficient, D , is set to 10~(-10) m~2/s for simulating two-fluid diffusion-convection flow, the mixing efficiency and the pressure drop of microchannel are investigated with various values of the angle of inclination, aspect ratio (h=αH) of obstacle and Reynolds number. When the flow passes through on the obstacles, rotation flow is observed. This flow pattern is repeated at each cycle. Besides, in each case that obstacles are turned to the center of channel and to the side walls, rotational direction is changed reversely. In case of pressure drop, as the Reynolds number, the angle of obstacle (θ) and the aspect ratio (α ) are increased, the pressure drop is also increased. Results show that the ratio between the maximum and minimum of pressure drop is the order-of-magnitude of 1 at Re= 1.667. Results also show that the angle of inclination of obstacles has more influence on the mixing performance than the height of obstacles and Reynolds number.
机译:微通道中两种或更多种流体流的混合需要相当长的通道长度。因此,为了提高混合性能,在通道中放置了障碍物以扰乱流动并减小扩散路径。流速场的破坏改变了从一种流体到另一种流体的流动方向。适当设计的几何参数,例如布局,与主流方向的角度以及障碍物的纵横比,将导致混合性能的改善,而压降的增加很少。在这项研究中,使用了T型矩形微通道,它有两个W×H×L = 100×100×1000μm〜的入口和一个W×H×L = 200×100×6950μm〜3的出口。此外,混合通道具有障碍物,该障碍物以倾斜角度并且在下层上以尺寸W×H×L = 10×100×hμm〜3放置。为了估计混合性能,用水和乙醇进行了数值分析。特别是将扩散系数D设置为10〜(-10)m〜2 / s以模拟双流体扩散-对流流动,研究了不同角度下的微通道混合效率和压降。倾斜度,障碍物的纵横比(h =αH)和雷诺数。当流经过障碍物时,观察到旋转流。在每个循环中重复这种流动方式。此外,在障碍物分别转向通道中心和侧壁的情况下,旋转方向相反地改变。在压力下降的情况下,随着雷诺数,障碍物的角度(θ)和纵横比(α)增加,压力下降也增加。结果表明,在Re = 1.667时,最大和最小压降之比为1的数量级。结果还表明,障碍物的倾斜角度比障碍物的高度和雷诺数对混合性能的影响更大。

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